EP2367888A1 - Granulats à pigments - Google Patents
Granulats à pigmentsInfo
- Publication number
- EP2367888A1 EP2367888A1 EP09799537A EP09799537A EP2367888A1 EP 2367888 A1 EP2367888 A1 EP 2367888A1 EP 09799537 A EP09799537 A EP 09799537A EP 09799537 A EP09799537 A EP 09799537A EP 2367888 A1 EP2367888 A1 EP 2367888A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- pigment granules
- pigment
- pigments
- granules according
- granules
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
Classifications
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C1/00—Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C1/00—Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
- C09C1/0015—Pigments exhibiting interference colours, e.g. transparent platelets of appropriate thinness or flaky substrates, e.g. mica, bearing appropriate thin transparent coatings
- C09C1/0024—Pigments exhibiting interference colours, e.g. transparent platelets of appropriate thinness or flaky substrates, e.g. mica, bearing appropriate thin transparent coatings comprising a stack of coating layers with alternating high and low refractive indices, wherein the first coating layer on the core surface has the high refractive index
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C1/00—Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
- C09C1/0081—Composite particulate pigments or fillers, i.e. containing at least two solid phases, except those consisting of coated particles of one compound
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C3/00—Treatment in general of inorganic materials, other than fibrous fillers, to enhance their pigmenting or filling properties
- C09C3/04—Physical treatment, e.g. grinding, treatment with ultrasonic vibrations
- C09C3/045—Agglomeration, granulation, pelleting
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D5/00—Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
- C09D5/03—Powdery paints
- C09D5/032—Powdery paints characterised by a special effect of the produced film, e.g. wrinkle, pearlescence, matt finish
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D5/00—Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
- C09D5/03—Powdery paints
- C09D5/033—Powdery paints characterised by the additives
- C09D5/035—Coloring agents, e.g. pigments
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D5/00—Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
- C09D5/36—Pearl essence, e.g. coatings containing platelet-like pigments for pearl lustre
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D7/00—Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
- C09D7/40—Additives
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H19/00—Coated paper; Coating material
- D21H19/36—Coatings with pigments
- D21H19/38—Coatings with pigments characterised by the pigments
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/60—Particles characterised by their size
- C01P2004/61—Micrometer sized, i.e. from 1-100 micrometer
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C2200/00—Compositional and structural details of pigments exhibiting interference colours
- C09C2200/10—Interference pigments characterized by the core material
- C09C2200/1004—Interference pigments characterized by the core material the core comprising at least one inorganic oxide, e.g. Al2O3, TiO2 or SiO2
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C2200/00—Compositional and structural details of pigments exhibiting interference colours
- C09C2200/10—Interference pigments characterized by the core material
- C09C2200/102—Interference pigments characterized by the core material the core consisting of glass or silicate material like mica or clays, e.g. kaolin
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C2200/00—Compositional and structural details of pigments exhibiting interference colours
- C09C2200/10—Interference pigments characterized by the core material
- C09C2200/1054—Interference pigments characterized by the core material the core consisting of a metal
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C2200/00—Compositional and structural details of pigments exhibiting interference colours
- C09C2200/30—Interference pigments characterised by the thickness of the core or layers thereon or by the total thickness of the final pigment particle
- C09C2200/301—Thickness of the core
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C2200/00—Compositional and structural details of pigments exhibiting interference colours
- C09C2200/30—Interference pigments characterised by the thickness of the core or layers thereon or by the total thickness of the final pigment particle
- C09C2200/302—Thickness of a layer with high refractive material
Definitions
- Pigmentation of application media in particular paints, plasters, lacquers, powder coatings, plastics and as scattering granules, e.g. for decoration of wallpaper.
- plastics e.g. nonpolar thermoplastics based on polyolefins, e.g. Polyethylene, polypropylene, without pretreatment methods, e.g. Corona discharge or flame,
- Pigment granules with plastic supports preferably polyolefins and / or glass, which do without additional pretreatment and do not have the disadvantages of the prior art mentioned above.
- pigment granules based on a carrier material such as e.g. Polymer particles, glass beads or hollow glass spheres or mixtures thereof, which are coated with one or more platelet-shaped effect pigments, are very well suited for economical and sustainable permanent coating.
- the present invention therefore relates to pigment granules based on a carrier material which is coated by means of an adhesion promoter with one or more platelet-shaped effect pigments.
- the effect pigment is preferably on the surface with the support, e.g. a polymer particle, a glass ball or glass hollow sphere, glued or partially or completely coated.
- the present invention further describes a one-step process for the preparation of the pigment granules according to the invention, which is based on the direct coating of the support materials, wherein the proportion of effect pigments on the support surface is generally ⁇ 50% by weight. Since the process of the invention is not bound to a thermoplastic or duroplastic carrier plastic, but is a carrier-independent process, this process is also considered to be particularly economical.
- the present invention furthermore relates to a process for the preparation of the pigment granules according to the invention, wherein one or more platelet-shaped effect pigments, at least one adhesion promoter and optionally additives are mixed with the support material.
- the pigment granules according to the invention are particularly suitable for use as scattering granules in effect wallpapers, for structural plaster systems and textile coatings.
- the pigment granules of the invention are not dusty and very free-flowing, which reduces the expenditure on equipment in their processing.
- An essential constituent of the pigment granules according to the invention is, in addition to the effect pigment, the carrier material.
- a suitable carrier material should in particular have a high transparency.
- Transparent supports e.g. Plastic particles, glass spheres and hollow glass spheres, with their translucency, support the optical properties, e.g. the pearlescent or metallic luster, the effect pigments applied to the surface.
- the carrier materials are present as individual particles, which are preferably spherical.
- the carrier material preferably has particle sizes of
- Suitable support materials are preferably polymer particles, glass full spheres and glass hollow spheres.
- polymer particles are preferably those of plastic (e), such as. Thermoplastics or thermosets, for use.
- the polymer particles are preferably composed of polyolefins, in particular polyethylene (PE) and polypropylene (PP), polystyrene (PS), polymethyl methacrylate (PMMA), polyethylene terephthalate (PET), polycarbonate (PC), polyvinyl acetate copolymer (PVAC), polyvinyl chloride ( PVC)
- EAA Ethylene acrylic acid copolymer
- PVA polylactic acid
- Particularly preferred support materials are composed of EAA (ethylene-acrylic acid copolymer), eg available from the Fa. ExxonMobil under the trade name Escor TM, or EVA (ethylene vinyl acetate copolymer), for example, Evatane ® 24-03 by the company.
- Escor TM ethylene-acrylic acid copolymer
- EVA ethylene vinyl acetate copolymer
- Evatane ® 24-03 by the company.
- ARKEMA or of polyvinyl acetate (PVAC), for example Vinnaperl 10 or Vinnaperl 20 from Wacker Chemie.
- the carrier material is preferably spherical. It preferably has a particle size of 0.05-50 mm, in particular 0.5-10 mm, very particularly preferably 0.5-5 mm.
- the commercially available plastic powders or plastic granules often have particle sizes of 1 to 5 mm. These polymer particles must then be previously melted for use in the preparation of the pigment granules of the invention and then, for example, by granulation, e.g. Underwater granulation, and grain size adjustment, e.g. B. by means of a perforated disc, can be adjusted to the desired particle size and shape.
- granulation e.g. Underwater granulation
- grain size adjustment e.g. B. by means of a perforated disc
- spherical microgranules of 0.5 -1 mm which consist of LD-PE (low density polyethylene) or HD-PE (high-density polyethylene), as this example, the Fa.
- the polymer particles are preferably spherical and have a particle size of 0.05-5 mm, in particular 0.05-2 mm, very particularly preferably 0.05-1 mm. It is also possible to use unstructured particles of the same particle size distribution.
- Rotational molding is understood to mean the production of plastic hollow bodies after spin-spinning using a biaxial rotational movement.
- Glass carrier beads or hollow glass beads may also be used as carrier material, preferably particle sizes of 0.3-50 mm, in particular from 0.5 to 10 mm, very particularly preferably from 0.5 to 5 mm.
- Such glass beads are commercially available, for example from the Fa. Sovitec GmbH.
- the glass beads should be chemically resistant depending on the application.
- glass beads or glass hollow spheres of soda lime glass main components: SiO 2 / CaO / Na 2 O), ECR glass, C glass Borosilakatglas or quartz glass are used.
- Mixtures of different carrier materials may also be used, e.g.
- the carrier materials are mixed in such a way that physical and chemical properties, such as adhesion in the application medium and chemical resistance, correlate with aesthetic effects and economic considerations.
- carrier material mixtures are binary mixtures which can be mixed with each other in any ratio.
- the ratio is preferably 1: 1 to 1:10 or 10: 1.
- a carrier material and blowing agent-additive-thermoplastic plastic particles can be used, provided that they are in the
- Pigment granules on Such support materials can be used in particular in the design of textured wallpaper.
- Suitable adhesion promoters are preferably those which physically dry c. Particularly preferred as adhesion promoter aqueous
- Emulsions are used, preferably EAA emulsions (ethylene acrylic acid copolymer), commercially available, for example, from Messrs. Michelman under the name "Michem Prime 4983 R” and emulsions and dispersions based on acrylated polypropylenes or low chlorinated polypropylenes. Such emulsions and dispersions are commercially available, for example from the Fa.
- EAA emulsions ethylene acrylic acid copolymer
- Tramaco under the designation “Trapylen 9310 W” and “Trapylen 6700 W”.
- the size of the EAA emulsion is preferably 20-300 nm, the EAA emulsions preferably used are preferably composed of 65-85 parts of water and 15 parts EAA 15-35..
- the size of the acrylated polypropylene or low chlorinated polypropylene emulsion particles or dispersion particles is preferably 50-5000 nm.
- Suitable adhesion promoters are also wax emulsions, commercially available, for example, from the company KEIM ADDITEC Surface GmbH.
- the wax emulsions preferably contain? F- emulsion of the size 20-100 nm.
- the appropriate wax emulsions preferably have a melting range of 50-160 0 C, especially 90-140 0 C and most preferably from 90-130 0 C. on.
- adhesion promoters are mentioned which are based on aqueous dispersions, such as for example those 1) based on copolymers or based on terpolymers:
- Vinyl chloride (VC) / ethylene [E] / vinyl laurate (VL) VC / EA / L
- Vinyl acetate (VAC) / (ethylene) [E] / vinyl chloride (VC) VAC / EA / C
- PVB polyvinyl butyral dispersions
- PE Polyether
- PU Polyurethane
- PC Polycarbonate
- PU Polyurethane
- Polyester PES / PC / PU
- Suitable adhesion promoters are furthermore adhesives based on resins and polymers which are dilutable or soluble in organic solvents. Examples of suitable raw materials can be found e.g. in Lackrohstofftabellen, Vincentz-Verlag, 10th edition, edition 2000, pages 62-622.
- the adhesives that can be used as adhesion promoters are subdivided according to the hardening mechanism in:
- Polymerization adhesives e.g.
- polycondensation adhesives e.g.
- hot melt adhesives e.g. Moisture-reactive amorphous poly alpha olefin hot melt adhesive
- the proportion of adhesion promoter in the pigment granules according to the invention is preferably from 0.05 to 20% by weight, in particular from 0.1 to 10% by weight, very particularly preferably from 0.15 to 5% by weight, based on the total mass of the pigment granules.
- the effect pigments, the support material and the adhesion promoter and optionally additives are mixed with one another.
- the carrier material with the effect pigment is at least partially or completely coated or enveloped by the emulsion.
- a complete coating and "gluing" of the carrier material with the platelet-shaped effect pigment is very particularly preferred.
- the flake-form effect pigments are preferably pearlescent pigments, interference pigments, metallic effect pigments, multilayer pigments with transparent, semitransparent and / or opaque layers, holographic pigments, coated or uncoated BiOCl pigments and / or LCP pigments.
- Pearlescent pigments, interference pigments, metallic effect pigments or multilayered pigments which can be used according to the present invention are based on transparent, semi-transparent and / or opaque layers
- platelet-shaped TiO 2 kaolin, talc, synthetic (eg fluorophlogopite) or natural mica, doped or undoped glass flakes, metal flakes, flaky SiO 2 , flaky Al 2 O 3 or platelet-shaped iron oxide are suitable.
- synthetic (eg fluorophlogopite) or natural mica doped or undoped glass flakes, metal flakes, flaky SiO 2 , flaky Al 2 O 3 or platelet-shaped iron oxide are suitable.
- metal plates may include aluminum, titanium, bronze, steel or silver, preferably aluminum and / or titanium
- the metal flakes may be passivated by appropriate treatment
- the glass flakes can be made of all known to those skilled glass types consist, for example from A.. Glass, E glass, C glass, ECR glass, waste glass, window glass, borosilicate glass, Duran® glass, laboratory glassware or optical
- the refractive index of the glass flakes is preferably 1.45-1.80, in particular 1.50-1.70.
- the glass substrates of C glass, ECR glass or borosilicate glass may be provided with one or more transparent semitransparent and / or opaque layers comprising metal oxides, metal oxide hydrates, metal suboxides, metals, metal fluorides, metal nitrides, metal oxynitrides or
- Metal oxide hydrate, metal suboxide, metal, metal fluoride, metal nitride, metal oxynitride layers or mixtures thereof may be low (refractive index ⁇ 1.8) or high refractive index (refractive index> 1.8).
- Suitable metal oxides and metal oxide hydrates are all metal oxides or metal oxide hydrates known to the person skilled in the art, such as, for example, For example, alumina,
- alumina hydrate silica, silica oxide, iron oxide, tin oxide, ceria, zinc oxide, zirconia, chromia, titania, especially titania, titania hydrate and mixtures thereof, e.g. Ilmenite or pseudobrookite.
- metal suboxides for example, the titanium suboxides can be used. Suitable metals are e.g. Chromium, aluminum, nickel, silver, gold, titanium, copper or alloys, as
- magnesium fluoride is suitable.
- metal nitrides or metal oxynitrides for example, the nitrides or oxynitrides of the metals titanium, zirconium and / or tantalum can be used. Preference is given to metal oxide, metal, metal fluoride and / or metal oxide hydrate layers and very particularly preferably metal oxide and / or
- Metal oxide hydrate, metal or metal fluoride layers are present, preferably alternating high and low refractive layers. Particular preference is given to layer packages of a high and a low refractive index layer, one or more layers being present on the support
- the sequence of high and low refractive index layers can be adapted to the carrier thereby to offset the carriers in the multi-layer structure with
- the metal oxide, metal oxide hydrate, metal suboxide, metal can.
- Metal fluoride, metal nitride, metal oxynitride layers may be mixed or doped with colorants as colorants or others
- organic or inorganic color pigments such as colored metal oxides, eg magnetite, chromium oxide or color pigments such as Berlin Blue, ultramarine, bismuth vanadate, Thenards Blue, or organic color pigments such as indigo, azo pigments, phthalocyanines or carmine red or elements such as yttrium or antimony. Effect pigments comprising these layers exhibit a wide variety of colors with respect to their body color and an angle-dependent change of color (color flop) may be due to interference in many cases, c.
- organic or inorganic color pigments such as colored metal oxides, eg magnetite, chromium oxide or color pigments such as Berlin Blue, ultramarine, bismuth vanadate, Thenards Blue, or organic color pigments such as indigo, azo pigments, phthalocyanines or carmine red or elements such as yttrium or antimony. Effect pigments comprising these layers exhibit a wide variety of colors with respect to their body color and an angle-dependent
- the outer layer on the support is in a preferred embodiment a high refractive index metal oxide.
- This outer layer may additionally be applied to the above-mentioned layer packages or to high-index carriers
- TiO 2 titanium suboxides, Fe 2 O 3 , Fe 3 O 4 , SnO 2 , ZnO, ZrO 2 , Ce 2 O 3 , CoO, Co 3 O 4 , V 2 O 5 , Cr 2 O 3 and / or mixtures thereof, such as ilmenite or pseudobrookite exist.
- TiO 2 is particularly preferred, further Fe 2 O 3 , as well as mixtures of TiO 2 and Fe 2 O 3 . If the support plates are coated with TiO 2 , the TiO 2 is preferably present in the rutile modification, further in the
- an SiO 2 layer can be applied as a protective layer to the substrate chip. If the substrate chip is a glass plate, it is often advisable to apply an SiO 2 layer in order to protect the glass plate against leaching in the case of the wet-chemical coating.
- high refractive index means a refractive index of> 1.8
- low refractive index means a refractive index of ⁇ 1.8.
- Metal fluoride, metal nitride, metal oxynitride or a mixture thereof is usually 3 to 300 nm and in the case of the metal oxide, metal oxide, metal, metal fluoride, metal nitride, metal oxynitride or a mixture thereof preferably 20 to 200 nm Metal layers is preferably 4 to 50 nm.
- Platelet-shaped supports and / or platelet-shaped supports coated with one or more transparent or semitransparent metal oxide, metal or metal fluoride layers generally have a thickness between 0.05 and 5 ⁇ m, in particular between 0.1 and
- the extension in the length or width is usually between 1 and 250 ⁇ m, preferably between 2 and 200 ⁇ m and in particular between 2 and 100 ⁇ m.
- TiO 2 / Fe 2 O 3 means that TiO 2 and Fe 2 O 3 are present in one layer as a mixture and / or as a mixed oxide in the form of the pseudobrookite.
- Pseudobrookite or the TiO 2 / Fe 2 O 3 mixed layer may optionally also be doped with Al 2 O 3 .
- Suitable effect pigments are commercially available, for example from BASF Corp. For example, under the brand names Fire Mist ®, TM Rightfit, Magna Pearl ®, from Merck KGaA under the trade name Iriodin ®, Miraval ®, Xirallic ® and ColorStream ®.
- the proportion by weight of the platelet-shaped effect pigments in the pigment granules according to the invention is generally between 0.1 and 50% by weight, preferably between 0.5 and 30% by weight, very particularly preferably between 1 and 10% by weight, based on the pigment granules.
- the optimum proportions are easy to determine for a person skilled in the art and depend essentially on the particle size of the effect pigments used, the form factor of the effect pigments and the type of pigment buildup.
- Particularly preferred pigment granules according to the invention contain
- the total amount of all components in the pigment granules is ⁇ 100% by weight.
- effect granules which contain the smallest possible proportion ( ⁇ 10% by weight) of the relatively expensive effect pigments and a high proportion (> 50% by weight) of inexpensive carrier material.
- This preferred embodiment is particularly interesting in the scatter application of the granules of effect wallpaper. 15
- the pigment granules according to the invention may contain further additives, such as are suitable for use in application media in the fields of paints, lacquers, powder coatings,
- Such additives and / or adjuvants may include lubricants, release agents, stabilizers, antistatic agents, flame retardants, antioxidants, colorants, such as dyes, inorganic color pigments and / or organic color pigments, flexibilizers, plasticizers, such as diisononyl phthalate, adhesion promoters, blowing agents, antioxidants, UV absorbers , inorganic fillers and / or surfactants, organic
- the pigment granules of the invention contain wetting agents, e.g. Silicones, silanes and / or fluorosurfactants.
- wetting agents e.g. Silicones, silanes and / or fluorosurfactants.
- the pigment granules according to the invention can be produced relatively easily.
- Possible first 11 methods are the gentle mixture of the individual components-effect pigment (s), carrier material, adhesion promoter-and subsequent rotogranulation.
- the components to be mixed with a mixer in which the
- the granules are rounded to the intended particle size on a horizontally rotating pelletizing plate.
- the gentle drying of the raw granules takes place in a fluidized bed, e.g. in a fluidized bed or fluidized bed dryer. However, preference is given to the embodiment in a fluidized-bed dryer.
- Adhesive the carrier material and optionally additives is mixed. This embodiment is particularly preferred.
- the invention also provides a process for the preparation of the pigment granules according to the invention, which is characterized in that one or more platelet-like effect pigments, the or the support material (a) with at least one adhesion promoter and optionally one or more additives are mixed simultaneously or sequentially ,
- the pigment granules according to the invention are characterized by being abrasion-resistant, dimensionally stable and having a uniform color effect.
- granules are all solid particle shapes conceivable in the art, such as e.g. Pellets, briquettes, pearlets,
- the particle sizes of the granules are preferably in the range of 0.05 to 150 mm, in particular 0.1 to 20 mm, and most preferably in the range of 0.1 to 6 mm.
- the granules according to the invention preferably contain
- the coating process produces such a directed structure of the employed platelet effect pigments (or mixtures) in the finished granules that the low pigment loading noted in the invention achieves similar effects that would otherwise produce the prior art granules having effect pigment levels> 50%.
- PU polyurethane
- the present invention also relates to the use of the pigment granules of the invention in paints, lacquers, printing inks, plastics, and as scattering granules, e.g. for wallpaper, as well as the use in hydraulic curing effect plaster systems.
- the present invention furthermore relates to the use of the pigment granules according to the invention in plastics applications, in particular rotary molding.
- Example 1 Support material: PVAC particles
- the pigment granules according to the invention For the preparation of the pigment granules according to the invention, a homogeneous mixing is to be ensured.
- the mixture is made using an Eirich R02 mixer.
- Vinnaperl 10 1000 g Vinnaperl 10 (PVAC particles of particle size 0.5-1 mm of Fa.
- Iriodin 305 ® multilayer pigment from Merck;. With TiO 2, Fe 2 O 3 and SiO 2 coated mica flakes) are in Mixing container presented and mixed (plate / whirler). Then 55 g of Michem Prime 4990 R (35% EAA emulsion from Michelman Inc.) are added slowly. The mixture is then mixed homogeneously (plate / whirler).
- the moist pigment / polymer / plastic mixture produced in this way is pelleted on an Eirich pelletizing plate TR 04. There, the size distribution is set.
- Target grain size set. If the nominal grain size is set, the batchwise entry of the total amount of the water-wet pigment / polymer / plastic batch is started.
- the nominal size is particularly controlled by the dimension (size expansion in mm) of the plastic granules used and should increase in the given experiment to 2 ⁇ 0.5 mm.
- portions between 50-100 g are entered, which can be added within a short time (1 kg about 10-15 min).
- Coarser aggregates accumulate in the middle of the "material flow kidney” produced during pelleting. These are picked up with a small shovel, crushed by hand and added again.
- the moist, granulated mixture is at 40 - 60 ° C in a fluidized bed dryer for 10-60 min. dried.
- the granules produced in this way are classified as safe by a sieve of mesh size 3.55 mm.
- Example 2 Support material: glass solid beads
- the pigment granules according to the invention For the preparation of the pigment granules according to the invention, a homogeneous mixing is to be ensured.
- the mixture is prepared with the aid of an Eirich R02 mixer.
- Vialux SB 20 solid glass beads of particle size 0.6-1, 4 mm of Fa. Sovitec GmbH
- Iriodin ® 305 10.0 g Iriodin ® 305 are placed in the mixing container and mixed (Plates / swirler). Thereafter, 5 g of Michem Prime 4983 R (25% EAA emulsion from Michelman Inc.) are added. Subsequently, the mixture is mixed homogeneously (plate / whirler).
- the moist pigment / polymer / glass bead mixture produced in this way is pelleted on an Eirich pelletizing plate TR 04. There, the size distribution is set. For this purpose, 200 g of freshly prepared granules are placed on the plate and set at 200-350 U / min and a 15 tilt angle of 30-40 °, the target grain size. Is the
- Set desired grain size is started with the portionwise entry of the total amount of the water-moist effect pigment / polymer / plastic batch.
- the nominal size is especially determined by the dimension (size expansion in
- the moist, granulated mixture is at 40 - 60 ° C in a fluidized bed dryer for 10-60 min. dried.
- the granules produced in this way are classified by a sieve of mesh size 3.55 mm 30.
- the pigment granules obtained is resistant to abrasion, dimensionally stable and has an extraordinary purity of the pearl effect produced.
- Example 3 Alkali-resistant coating - carrier material: PE particles
- the pigment granules according to the invention For the preparation of the pigment granules according to the invention, a homogeneous mixing is to be ensured.
- the mixture is made using an Eirich R02 mixer.
- the moist pigment / polymer / plastic mixture produced in this way is pelleted on an Eirich pelletizing plate TR 04. There, the size distribution is set.
- Target grain size set If the nominal grain size is set, the portion-wise entry of the total amount of the water-moist effect pigment / polymer / plastic batch is started.
- the nominal size is particularly controlled by the dimension (size expansion in mm) of the plastic granules used and should increase in the given experiment to 5.5 ⁇ 0.5 mm. In this case, portions between 50-100 g are entered, which can be added within a short time (1 kg about 10-15 min). Coarser aggregates accumulate in the middle of the "material flow kidney" produced during pelleting. These are picked up with a small shovel, crushed by hand and added again.
- the moist, granulated mixture is at 40 - 60 0 C in a fluidized bed dryer for 10-60 min. dried. The granules produced in this way are classified as safe by a sieve of mesh size 6.5 mm.
- the pigment granules obtained is resistant to abrasion, dimensionally stable and has an extraordinary purity of the pearl effect produced.
- the produced effect granules also have an alkaline strength according to DIN EN ISO 175 (precast part test).
- Example 4 Carrier material: PE particles
- the pigment granules according to the invention For the preparation of the pigment granules according to the invention, a homogeneous mixing is to be ensured.
- the mixture is made using an Eirich R02 mixer.
- the moist pigment / polymer / plastic mixture produced in this way is pelleted on an Eirich pelletizing plate TR 04. There, the size distribution is set. For this purpose, 200 g of freshly prepared granules are placed on the plate and set at 200-350 U / min and an inclination angle of 30-40 °, the target grain size. If the nominal grain size is set, the batchwise entry of the total amount of the water-wet pigment / polymer / plastic batch is started.
- the target size is particularly controlled by the dimension (size expansion in mm) of the plastic granules used and should increase in the given experiment to 5.5 ⁇ 0.5 mm.
- portions between 50-100 g are registered, which within a short time can be added (1 kg about 10-15 min).
- Coarser aggregates accumulate in the middle of the "material flow kidney” produced during pelleting. These are picked up with a small shovel, crushed by hand and added again.
- the moist, granulated mixture is at 40 - 60 0 C in one
- the granules produced in this way are classified as safe by a sieve of mesh size 6.5 mm.
- the pigment granules obtained is resistant to abrasion, dimensionally stable and has an extraordinary purity of the pearl effect produced.
- Example 5 Support Material: Full Glass Beads
- the pigment granules according to the invention For the preparation of the pigment granules according to the invention, a homogeneous mixing is to be ensured.
- the mixture is made using an Eirich R02 mixer.
- Vialux coated SB 20 solid glass beads of particle size 0.6-1, 4 mm of Fa. Sovitec GmbH
- 10.0 g Colorstream ® Arcticfire with TiO 2
- the moist pigment / polymer / glass bead mixture produced in this way is pelleted on an Eirich pelletizing plate TR 04. There will be the
- Size distribution set For this purpose, 200 g of freshly prepared granules are placed on the plate and set at 200-350 U / min and an inclination angle of 30-40 °, the target grain size. If the nominal grain size is set, the portionwise entry of the total amount of the water-moist effect pigment / polymer / plastic batch is started.
- the target size is particularly controlled by the dimension (size expansion in mm) of the glass beads used and should increase in the given experiment to 2 ⁇ 0.5 mm.
- portions between 50-100 g are added, which can be added within a short time c (1 kg about 10-15 min).
- Coarser aggregates accumulate in the middle of the "material flow kidney" produced during pelleting. These are picked up with a small shovel, crushed by hand and added again.
- the moist, granulated mixture is at 40 - 60 0 C in a 10 fluid bed dryer for 10-60 min. dried.
- the granules produced in this way are classified as safe by a sieve of mesh size 3.55 mm.
- the pigment granules obtained is resistant to abrasion, dimensionally stable and has an extraordinary purity of the pearl effect produced. 15
- the moist pigment / polymer / plastic mixture prepared in this way is pelleted on an Eirich pelletizing plate TR 04. There will be the
- Size distribution set For this purpose, 200 g of freshly prepared granules are placed on the plate and at 200-350 U / min and a Inclination angle of 30-40 ° set the target grain size. If the nominal grain size is set, the batchwise entry of the total amount of the water-wet pigment / polymer / plastic batch is started.
- the target size is particularly controlled by the dimension (size expansion in mm) of the plastic granules used and should increase in the given experiment to 5.5 ⁇ 0.5 mm. In this case, portions between 50-100 g are entered, which can be added within a short time (1 kg about 10-15 min). Coarser aggregates 10 accumulate in the middle of the "material flow kidney” produced during pelleting. These are picked up with a small shovel, crushed by hand and added again.
- the moist, granulated mixture is at 40 - 60 0 C in a fluidized bed dryer for 10-60 min. dried.
- the 15 granules produced in this way are classified as safe by a sieve of mesh size 6.5 mm.
- the pigment granules obtained is resistant to abrasion, dimensionally stable and has an extraordinary purity of the pearl effect produced.
- Carrier material PE particles
- the carrier plastic powder Borecene LLD RM 7243 (LLD-PE plastic powder from Borealis) is microgranulated to the particle diameter 0.6-1 mm in an underwater granulation prior to the start of the test using an ?
- the measure serves to produce a uniform carrier surface for subsequent coating by means of effect pigments on the plastic carrier surface.
- the pigment granules For the preparation of the pigment granules according to the invention a homogeneous mixing is to be ensured.
- the mixture is made using an Eirich R02 mixer.
- 901 g Borecene LLD RM 7243 microgranules (LLD-PE plastic / LLD. Linear low density Fa Borealis) the particle size of 0,5 - 1 mm and 28.50 g of Iriodin 305 ® (. Pearlescent pigment from Merck) are used in Mixing container presented and mixed (plate / whirler). Then slowly 71, 5 g Ultralaube XP-06070480 (42% LDPE-Emulison the Fa.
- the moist pigment / polymer / plastic mixture produced in this way is pelleted on an Eirich pelletizing plate TR 04. There, the size distribution is set. For this purpose, 200 g of freshly prepared granules are placed on the plate and set at 200-350 U / min and an inclination angle of 30-40 °, the target grain size. If the nominal grain size is set, the batchwise entry of the total amount of the water-wet pigment / polymer / plastic batch is started. The nominal size is particularly controlled by the dimension (size expansion in mm) of the plastic granules used and should increase in the given experiment to 1, 5-2 mm.
- portions between 50-100 g are entered, which can be added within a short time (1 kg about 10-15 min).
- Coarser aggregates accumulate in the middle of the "material flow kidney” produced during pelleting. These are picked up with a small shovel, crushed by hand and added again.
- the moist, granulated mixture is dried at 40 - 60 0 C in a fluidized bed dryer for 10-60 min.
- the granules produced in this way are classified as safe by a sieve of mesh size 2.5 mm.
- the pigment granules obtained is resistant to abrasion, dimensionally stable and has an extraordinary purity of the pearl effect produced.
- the support materials of the granules of the invention are that a
- Loss of effect pigment coating on the substrate decreases. It is thereby possible to create relief-like structures on the surface of the effect granulate paper or nonwoven surface.
- An additional advantage of embossing arises in the increase of the mechanical resistances, such as the abrasion resistance of the effect granules surface produced.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Wood Science & Technology (AREA)
- Composite Materials (AREA)
- Paints Or Removers (AREA)
- Pigments, Carbon Blacks, Or Wood Stains (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE200810064201 DE102008064201A1 (de) | 2008-12-22 | 2008-12-22 | Pigmentgranulate |
PCT/EP2009/009101 WO2010072376A1 (fr) | 2008-12-22 | 2009-12-18 | Granulats à pigments |
Publications (1)
Publication Number | Publication Date |
---|---|
EP2367888A1 true EP2367888A1 (fr) | 2011-09-28 |
Family
ID=41652058
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP09799537A Withdrawn EP2367888A1 (fr) | 2008-12-22 | 2009-12-18 | Granulats à pigments |
Country Status (8)
Country | Link |
---|---|
US (1) | US8883879B2 (fr) |
EP (1) | EP2367888A1 (fr) |
KR (1) | KR101792264B1 (fr) |
CN (1) | CN102264846B (fr) |
DE (1) | DE102008064201A1 (fr) |
EA (1) | EA026672B1 (fr) |
UA (1) | UA107922C2 (fr) |
WO (1) | WO2010072376A1 (fr) |
Families Citing this family (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE202010005960U1 (de) * | 2010-04-21 | 2010-10-28 | Creafurnish Ltd. | Multifunktionaler Putz |
CN103108922B (zh) * | 2010-09-15 | 2015-10-07 | 默克专利股份有限公司 | 颜料颗粒 |
US20150202557A1 (en) * | 2012-01-26 | 2015-07-23 | Ag+ Aps | Method for producing a filter element |
DE102012102165A1 (de) | 2012-03-14 | 2013-10-02 | Eckart Gmbh | Kompositpartikel, Verfahren zu deren Herstellung und Verwendung derselben |
DE102012103976A1 (de) * | 2012-05-07 | 2013-11-07 | Hd Kunststoffe & Kunststofferzeugnisse Gmbh | Polypropylen für das Rotationsformen |
CN103966920A (zh) * | 2014-04-11 | 2014-08-06 | 王兆进 | 一种带有亚克力珠的墙纸的加工方法 |
CN104234356A (zh) * | 2014-08-01 | 2014-12-24 | 王兆进 | 一种硅藻泥亚克力珠墙纸的制作方法 |
CN105825943A (zh) * | 2014-08-27 | 2016-08-03 | 周杰 | 电力发光电缆 |
CN105825942A (zh) * | 2014-08-27 | 2016-08-03 | 周杰 | 电力电缆 |
CN104347176B (zh) * | 2014-08-27 | 2016-08-24 | 国网山东省电力公司沂源县供电公司 | 一种发光电缆 |
CN104452476B (zh) * | 2014-12-12 | 2016-10-26 | 广东玉兰集团股份有限公司 | 一种金沙墙纸及其制备方法 |
US20200238579A1 (en) * | 2015-12-18 | 2020-07-30 | Merck Patent Gmbh | Process for the production of hollow plastic articles by rotational molding polymeric compounds in a rotomold |
CN106189371A (zh) * | 2016-07-11 | 2016-12-07 | 滁州格锐矿业有限责任公司 | 一种改性云母粉及其制备方法 |
CN106245455A (zh) * | 2016-08-24 | 2016-12-21 | 安徽中亚纸业有限公司 | 一种纸张用钛白色珠光染料及其制备方法 |
CA3068014A1 (fr) * | 2017-05-19 | 2018-11-22 | Honeywell International Inc. | Compositions contenant des formulations de copolymere destinees a ameliorer l'adherence sur des substrats a faible energie de surface |
DE102018207815A1 (de) * | 2018-05-18 | 2019-11-21 | Karl Wörwag Lack- Und Farbenfabrik Gmbh & Co. Kg | Mehrschichtige, farb- und/oder effektgebende Lackierung sowie Verfahren zur Bildung einer Basislackschicht |
CN109382289B (zh) * | 2018-10-17 | 2021-09-17 | 苏州扬子江新型材料股份有限公司 | 高耐候性变色龙彩涂板及其制备方法 |
BR112021017832A2 (pt) * | 2019-04-11 | 2021-11-30 | Basf Se | Composição de pigmento, uso de uma composição de pigmento, composições de moldagem, processo para preparar uma composição de pigmento, uso de uma composição de moldagem termoplástica e moldagem |
CN114656740B (zh) * | 2022-03-18 | 2023-10-31 | 金发科技股份有限公司 | 一种免喷涂效果颜料及其制备方法和应用 |
WO2024017885A1 (fr) | 2022-07-19 | 2024-01-25 | Sun Chemical Corporation | Pigments à effets avec brillance |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20040043147A1 (en) * | 2001-12-12 | 2004-03-04 | Findley Larry K | Color coated plastic pellets |
Family Cites Families (28)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3087828A (en) * | 1961-06-28 | 1963-04-30 | Du Pont | Nacreous pigment compositions |
CA957108A (en) | 1971-03-30 | 1974-11-05 | E. I. Du Pont De Nemours And Company | Pigments treated with methacrylatochromic chloride for improved humidity resistance |
DE2603211C2 (de) | 1976-01-29 | 1987-02-05 | Merck Patent Gmbh, 6100 Darmstadt | Verfahren zur Herstellung von pulverförmigen Perlglanzpigment-Zubereitungen |
FR2400423A1 (fr) * | 1977-08-15 | 1979-03-16 | Asahi Dow Ltd | Matiere en particules expansees en resine de polyolefine |
DE3151354A1 (de) | 1981-12-24 | 1983-07-07 | Merck Patent Gmbh, 6100 Darmstadt | Perlglanzpigmente, verfahren zu ihrer herstellung und ihre verwendung |
DE3211166A1 (de) | 1982-03-26 | 1983-09-29 | Merck Patent Gmbh, 6100 Darmstadt | Verfahren zur hydrophobierung von perlglanzpigmenten |
DE3235017A1 (de) | 1982-09-22 | 1984-03-22 | Merck Patent Gmbh, 6100 Darmstadt | Perlglanzpigmente |
DE3334598A1 (de) | 1983-09-24 | 1985-04-18 | Merck Patent Gmbh | Witterungsbestaendige perlglanzpigmente |
IT1256263B (it) | 1992-12-30 | 1995-11-29 | Bayer Italia Spa | Granulati di coloranti scorrevoli,chimicamente resistenti,loro preparazione e loro impiego |
DE4323914A1 (de) | 1993-07-16 | 1995-01-19 | Merck Patent Gmbh | Perlglanzpigment-Zubereitung |
US5455288A (en) * | 1994-01-26 | 1995-10-03 | Needham; Donald G. | Dustless color concentrate granules |
US5571851A (en) | 1994-01-28 | 1996-11-05 | J.M. Huber Corporation | Reinforcing fillers for plastics systems |
JP3577576B2 (ja) | 1995-04-10 | 2004-10-13 | メルク株式会社 | 表面処理剤、表面処理薄片状顔料及びその製造方法 |
US5688449A (en) * | 1995-10-02 | 1997-11-18 | Nitech Corporation | Method of forming and extruding an additive-coated resin composition |
US5759255A (en) | 1996-02-07 | 1998-06-02 | Engelhard Corporation | Pearlescent pigment for exterior use |
CA2302429A1 (fr) * | 1997-10-08 | 1999-04-15 | H.B. Fuller Licensing & Financing, Inc. | Granules d'adhesif thermofusible comportant un enrobage continu d'agent facilitant la granulation |
DE19820112A1 (de) | 1998-05-06 | 1999-11-11 | Eckart Standard Bronzepulver | Mit reaktiven Orientierungshilfsmitteln beschichtete Effektpigmente |
DE10046152A1 (de) * | 2000-09-15 | 2002-03-28 | Merck Patent Gmbh | Pigmentpräparation in Granulatform |
US6451102B1 (en) | 2000-05-04 | 2002-09-17 | Merck Patent Gmbh | Pigment modification improving handling characteristics |
US6245323B1 (en) | 2000-05-26 | 2001-06-12 | Engelhard Corporation | Bonded metal hydroxide-organic composite polymer films on particulate substrates |
DE10054344A1 (de) | 2000-11-02 | 2002-05-29 | Clariant Gmbh | Verwendung von gecoateten Pigmentgranulaten in elektrophotographischen Tonern und Entwicklern, Pulverlacken und Ink-Jet-Tinten |
DE10259246A1 (de) * | 2002-12-17 | 2004-07-01 | Merck Patent Gmbh | Anorganische sphärische Absorptionspigmente |
DE10337188A1 (de) | 2003-08-13 | 2005-03-10 | Merck Patent Gmbh | Pigmentpräparation für Kunststoffe |
DE10345647A1 (de) | 2003-10-01 | 2005-04-21 | Merck Patent Gmbh | Pigmentpräparation für Kunststoffe |
US20050113487A1 (en) | 2003-11-25 | 2005-05-26 | Engelhard Corporation | Masterbatch precursor |
US20070022907A1 (en) | 2004-11-23 | 2007-02-01 | Basf Catalysts Llc | Colored Masterbatch Precursor |
DE102006039913A1 (de) | 2006-08-12 | 2008-02-14 | Clariant International Limited | Hochgefüllte Farbmittelzusammensetzung zum Einfärben und Modifizieren olefinischer wie nichtolefinischer Kunststoffe |
DE102008064202A1 (de) * | 2008-12-22 | 2010-06-24 | Merck Patent Gmbh | Pigmentgranulate |
-
2008
- 2008-12-22 DE DE200810064201 patent/DE102008064201A1/de not_active Withdrawn
-
2009
- 2009-12-18 EA EA201100972A patent/EA026672B1/ru not_active IP Right Cessation
- 2009-12-18 US US13/141,529 patent/US8883879B2/en not_active Expired - Fee Related
- 2009-12-18 EP EP09799537A patent/EP2367888A1/fr not_active Withdrawn
- 2009-12-18 WO PCT/EP2009/009101 patent/WO2010072376A1/fr active Application Filing
- 2009-12-18 KR KR1020117017127A patent/KR101792264B1/ko active IP Right Grant
- 2009-12-18 UA UAA201109112A patent/UA107922C2/ru unknown
- 2009-12-18 CN CN200980151760.XA patent/CN102264846B/zh not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20040043147A1 (en) * | 2001-12-12 | 2004-03-04 | Findley Larry K | Color coated plastic pellets |
Non-Patent Citations (1)
Title |
---|
See also references of WO2010072376A1 * |
Also Published As
Publication number | Publication date |
---|---|
CN102264846A (zh) | 2011-11-30 |
EA026672B1 (ru) | 2017-05-31 |
CN102264846B (zh) | 2014-06-04 |
EA201100972A1 (ru) | 2012-01-30 |
US8883879B2 (en) | 2014-11-11 |
WO2010072376A1 (fr) | 2010-07-01 |
KR20110100292A (ko) | 2011-09-09 |
UA107922C2 (en) | 2015-03-10 |
US20110301273A1 (en) | 2011-12-08 |
KR101792264B1 (ko) | 2017-11-01 |
DE102008064201A1 (de) | 2010-06-24 |
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